System and method for continuous strand fiberglass media processing

ABSTRACT

Accordingly, there is provided a method of manufacturing continuous strand fiberglass of progressive density with varying skins having steps of melting glass media into molten glass within a temperature controlled melter, molten glass exits melter through orifices of a bushing plate, of varying orifice row configurations, orienting the bushing plate 6 degrees relative to the axis of the drum. Rollers spread fibers, a temperature control system controlling reservoir binder temperature, and water spray nozzles control fiberglass moisture. A rotating drum, circumferentially and longitudinally superior in size has a substantial and sustainable control of the rotation of the drum. In another aspect, a method of forming a fiberglass mat, having the steps of feeding a fiberglass media between bowed rollers of providing for a differential pressure across the mat reducing weight variation with controllers integrally controlled by a computer machine.

This disclosure relates to a system, method and apparatus of manufacturing fiberglass and more particularly relates to an improved process of manufacturing fiberglass and an apparatus for improving the quality, efficiency and cost of manufacturing fiberglass.

BACKGROUND OF THE INVENTION

This disclosure in particular relates to an improved selection of raw materials input, involving the use of recycled cullet screened and vibrated, as well as a specially mixed and controlled resin with the addition of aqueous solutions and an improved apparatus for melting the fiberglass, sometimes referred to as the melter furnace, the plate (bushing) with perforations (orifices) for exiting the molten fiberglass from the melter, a temperature control assembly controlling temperature of the Urea Formaldehyde (UF) Resin and filament strands exiting the orifices of the bushing plate, in combination with an aqueous solution spray through a spray assembly and binder(s) through a binder spray assembly, which sprays various additives and control chemicals onto the fiberglass to adjust its properties as it winds onto a rotating drum, and the ability to spray various aqueous solutions onto the rotating drum in a specified manner covering the fiberglass mat deposited and varying configurations of roller assemblies utilizing portable devices with catch basins that control water spray, and with various chemicals and control systems (software and computers) provides for increased efficiency, quality, production capacity and in particular the creation of progressive densities of a fiberglass mat manufactured from a filament strand manufacturing process.

Subsequent improvements and variations of the Modigliani process have been made and are known in the art. Modigliani and progeny generally involve a melting furnace feeding molten glass which discharges fine glass fibers. These fine glass fibers are short in nature and not continuously fed and are in turn wrapped around a rotating drum in a random fashion. Moisture is measured on the fiberglass mat. In Modigliani and progeny, during the deposition of the fibers on the rotating drum, solutions are applied to the surface of the glass media mat. Technology for making glass fiber strands is known in the art. Such technology is described in several patents issued to Modigliani, namely, U.S. Pat. Nos. 2,546,230; 2,609,320 and 2,964,439 and several mentioned thereafter. Modigliani and progeny have done little to improve upon the efficiency of the manufacturing methods and apparatus either through new control methods or through process changes and nothing to adjust densities of fiberglass states to improve both surface and bulk characteristics of the fiberglass as deposited.

The present disclosure relates to improvements to the Modigliani patents and progeny that substantially change the initial conditions and ultimate quality of the fiberglass mat, improving upon the manufacturing process, providing for a different machine and process combination and creating the capability of providing progressive density fiberglass.

It would be advantageous to provide a system of manufacturing fiberglass that increases efficiency in production.

It would also be advantageous to provide a method of manufacturing fiberglass that utilizes a specific orientation of the bushing plate to the drum.

It would further be advantageous to decrease weight variations of the fiberglass mat by using load cells to increase the accuracy of the measurement of the weight variations.

It would further be advantageous to adjust the skin of the fiberglass media by passing the fiberglass media through a roller assembly having either straight or bowed rollers or in some embodiments both with a defined angular rotation that provide differential pressure across the mat reducing weight variations across the media and providing for more consistent water content improving the quality of the top and bottom skins (surfaces) of the fiberglass media as well as creating progressive densities substantially improving the bulk and surface characteristics of the fiberglass.

It would further be advantageous to utilize load cells to decrease weight variations of the mat and increase the accuracy of the final weight which improves product quality and increase accuracy to + or −5%.

It would also be advantageous to apply water by spraying it onto a flat surface of the fiberglass mat immediately prior to curing which results in a more consistent application of water resulting in higher quality skins and/or which in combination with the use of the bowed rollers results in the production of higher quality skins.

It would further be advantageous to apply water in combination with the binder as the binder is applied to the fiberglass on the rotating drum.

It would also be advantageous to apply water in combination with the binder for controlling the moisture content range to 36%-40% content by weight.

It would further be advantageous to control binder temperature range to 70 degrees Fahrenheit plus or minus 10% of the 70 degrees.

It would also be advantageous to control densities of the fiberglass mat in order to provide progressive densities of a fiberglass mat.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 Side cutaway view of a melting furnace with natural gas flame and a glass feeder hopper mechanism.

FIG. 2 Front cutaway view of a bushing plate and a cooling loop on bottom of the glass melting furnace.

FIG. 3 Bottom view of hole placement on furnace bushing plate.

FIG. 4 Top view of uninstalled cooling loop.

FIG. 5 Top view of glass melting furnace angled above rotating drum.

FIG. 6 Side cutaway view of rotating drum with furnace above feeding strands of glass and binder spray nozzle and water spray nozzle on rear of drum.

FIG. 7 End view of rotating drum illustrating recess in drum used to facilitate cutting completed fiberglass mat from the drum.

FIG. 8 End view of straight rollers and their associated water spray nozzles and arrow showing direction of travel of fiberglass.

FIG. 9 End view of bowed rollers and associated water sprays and arrow indicating direction of travel of the fiberglass.

FIG. 10 Top view of straight rollers.

FIG. 11 Side cutaway view of curing oven with arrow indicating direction of travel of fiberglass.

FIG. 12 Side cutaway view of letoff table showing gas burners below travel of fiberglass and radiant heaters above fiberglass travel with arrow indicating direction of travel of fiberglass.

FIG. 13 Close up top view of holes in furnace bushing plate.

FIG. 14 Close up side cutaway view of holes in furnace bushing plate.

FIG. 15 Side view of uninstalled cooling loop.

FIG. 16 Side view of load cell and bearing of rotating drum

FIG. 17 Top view of bowed rollers.

DETAILED DESCRIPTION OF THE DRAWINGS

A complete understanding of the present invention may be obtained by reference to the accompanying drawings, when considered in conjunction with the subsequent, detailed description, in which:

FIG. 1 is a side cutaway view of a melting furnace with natural gas flame and a glass feeder hopper mechanism, stationary glass feeder, and vibrator, secondary chute into the traversing melter furnace, showing the traverse cart, the track and the set point controller. This figure details the relative position of the various main components of the melting furnace and its traverse mechanism, with glass hopper (10), glass feeder (12), vibrator (14), to a secondary chute (16), a melt furnace (18) a flame temperature sensor (20) and a traverse cart (22) for traversing the melter furnace with track (24) and set point controller (26) for feeding more glass in the melter furnace.

FIG. 2 is a front cutaway view of a bushing plate and a cooling loop assembly on bottom of the glass melting furnace, bushing cooling loop assembly (28) demonstrating its position relative to the melter furnace. The front view cutaway of the cooling loop assembly explains the function of the loop or coils quite well. The angle is 80 degrees relative to horizontal. The top seven layers of coil are composed of ¼ inch copper refrigeration tubing which carries chilled water. The bottom layer is ⅜ inch copper tubing perforated with side air holes 1/32 inch in diameter directed at the Inconel bushing plate. The cutaway details of cooling loop (32) that are composed of a single copper air coil that is ⅜ inch diameter for air entry to rapidly cool the glass filaments exiting the bushing plate for retarding the flow of glass through the bushing plate, combined with a series of ¼ inch copper tubing or coils carrying chilled water wrapped adjacent to and looped back one on the other as portrayed in the front cutaway view. There is an air inlet and there are air outlet orifices, a water inlet and a water outlet. The shields (34) are plates, typically metal, which surround the area below the bushing plate used to prevent ambient air flow from causing the filaments to collide as they exit the bushing plate orifices.

FIG. 3 is a bottom view of hole placement on furnace bushing plate detail for hole patterns with a 0.500 inch space between each set of patterns (86) and fine detail of the orifice patterns (40).

FIG. 4 is a top view of uninstalled cooling loop assembly (32) with detail of the larger diameter air coil entry (42). The top view demonstrates the loop assembly demonstrated by the race track shape that is a 3 inch interior width and 15 inches in length for the inside diameter while portraying the dimensional position of the coiled loops that transport the water used to control temperature of the fibers as they exit the bushing plate assembly.

FIG. 5 Top view of glass melting furnace angled above rotating drum demonstrates a traversing melt furnace indicating the length of the furnace traverse (44) with a tilt of a 6 degree angle (30). An outline of the drum can be seen below the angle of traverse of the melt furnace and the approximate positioning of the traverse track over the rotating drum as well as the approximate drop location of the exiting filaments from the underside of the traverse furnace.

FIG. 6 Side cutaway view of rotating drum with furnace above feeding strands of glass with water (50) and resin spray nozzles (48) on rear of drum, both attached to the traversing furnace as shown. The hollow steel drum rotates against the falling filaments as shown with the falling filaments aligned tangentially to the drum so the filaments just touch the drum at a point.

FIG. 7 End view of rotating drum illustrating a notch (54) recessed in drum used to facilitate cutting completed fiberglass mat from the drum which allows the operator to cut longitudinally across the width of the drum to remove the mat from the drum.

FIG. 8 End view of straight rollers and their associated water spray nozzles (56), which is composed of a high pressure dual pumping system, each of which provides water sprays either on the rollers or the media from either Pump A (64) to the top side of the top roller or Pump B (64), typically spraying water from Pump B to the underside of the rollers, to control the media upper and lower skin, and arrow showing direction of travel of fiberglass. Top rollers (58) are adjustable and separately driven with respect to bottom coasting roller (62), with multiple spray heads from each adjustable spray head assembly. Bottom roller (60) is adjustable and separately driven from the top roller (58). (65) is the total assembly from top to wheels.

FIG. 9 End view of bowed rollers and associated water sprays and arrow indicating direction of travel of the fiberglass. Each roller is sprayed with water fog nozzles (70). Attached to and integrated with the portable Bowed Roller Assembly is a catch basin (72) which has been removed for clarity that captures the water fogged onto the rollers from above and below. FIG. 10 Top view of straight rollers in a roller assembly which is comprised of a series of straight rollers driven separately by a top roller drive (74) and a bottom or lower roller drive (76), multiple spray heads (78) across the roller assembly to spray continually across the entire width of the roller assembly.

FIG. 11 Side cutaway view of curing oven (88) with arrow indicating direction of travel of fiberglass with mat fed into the curing oven through a conveyor system with an upper chain conveyor (82) and lower chain conveyor (80). The upper and lower chain conveyors move at slightly different speeds relative to each other to keep the mat from bunching and prevent stretching of the mat. The process parameters are controlled by a controller with a computer, software, temperature sensors, airflow sensors and individually heated zones, the first surrounding the upper chain conveyor (82) followed by the second (84).

FIG. 12 Side cutaway view of letoff table showing gas burners (92) below travel of fiberglass and radiant heaters (90) above fiberglass travel with arrow indicating direction of travel of fiberglass.

FIG. 13 Close-up top view of holes (38) in furnace bushing plate.

FIG. 14 Close-up side cutaway view of holes (36) in furnace bushing plate.

FIG. 15 Side view of uninstalled cooling loop details cooling coils (32) that are composed of a single cooper air coil (42) that is ⅜ inch diameter for air entry combined with a series of ¼ inch copper tubing cooling water coils wrapped adjacent to and looped back one on the other as portrayed in the side view).

FIG. 16 Side view of load cell (52) and bearing of rotating drum. The measurement of load cell is based on a readout from the load cell that is based on the weight of the filaments plus the weight of the resin minus the weight of the drum to achieve an accurate reflection of the weight based on the travel of the load cell caused by the applied filaments creating the mat resulting in both a weight measurement and an approximate density determination.

FIG. 17 Top view of bowed roller assembly. A straight roller (66) that first engages the mat to three bowed rollers (68) that engages the mat and is used to maintain optimal width expansion consisting of a straight roller (66) that first engages the mat to three bowed rollers (68). The fiberglass mat first slides over straight roller in the direction of travel of the mat in a clockwise direction over the top of the roller and then under the second roller which is bowed (first in a series of bowed rollers) (68) in a counterclockwise direction and then over the top of the third roller which is bowed in a clockwise direction, and then under the fourth roller, bowed in a counterclockwise direction, the movement of the mat over and under the rollers provides for linear expansion of the mat. The three bowed rollers (68) each of which are sprayed with water across the span of the bowed rollers on the side opposite the fiberglass mat.

For purposes of clarity and brevity, like elements and components will bear the same designations and numbering throughout the Figures.

SUMMARY OF THE PRESENT DISCLOSURE

In accordance with the present disclosure, there is provided, in one aspect, a method of manufacturing continuous strand fiberglass filaments having the steps of selecting raw material inputs utilizing a variety of select methods, including controlling fines, and turbidity of the glass cullet and the temperature of the resin and aqueous solutions, selecting and controlling through a temperature control system and a bushing cooling loop assembly and a PH monitoring system a selection of urea formaldehyde resins in some applications and styrene in other applications and the conditioning of aqueous solutions and melting glass into a molten state within a temperature-controlled melting furnace, with a feed-back set point for controlling level of the molten glass with molten glass filaments instead of fibers exiting the furnace through the orifices of a bushing plate at a specific relative angle and applying the aforementioned aqueous solutions onto the filaments exiting the orifices of the bushing plate onto a rotating drum at a specified width as the melting furnace traverses the longitudinal axis of the rotating drum at a specified angle of traverse and then to a let-off table and from the let-off table, through a series of Upper and Lower Skin Control Assemblies with both bowed and straight rollers in varying configurations with catch basins and integrally mounted pumps controlling moisture and together with aqueous sprays controlling progressive density of the fiberglass and a variety of skins and to the curing oven with specified temperature zones and dual speed chain control of speed through the curing oven and onto an accumulator and wind-up machine all under control of a positive feedback quality loop control system all providing the machine, processes and devices to manufacture progressive density fiberglass and progressive density fiberglass mats.

DETAILED DESCRIPTION

Raw material inputs are comprised of recycled glass cullet, urea formaldehyde (UF) resin or styrene resin and water. The recycled glass cullet is sorted for purity and clarity or turbidity which is screened to achieve maximum dimensions of ½ inch to 1¼ inches in size. The glass cullet is dropped from a glass hopper (10) on to a stationary glass feeder (12) that is then vibrated using a vibrator (14) to remove any fines or excess glass dust. The vibrated glass cullet is then dropped from the glass feeder (12) to a secondary chute (16) that feeds the furnace (18).

Additionally, urea formaldehyde resin as used in filter applications is mixed with a specific additive under shear mixer conditions. The urea formaldehyde (UF) resin is maintained at controlled temperatures around 72 degrees Fahrenheit by cooling and heating coils in the storage and dispensing tanks. The UF resin is agitated in both the storage and dispensing tanks with PH monitored continually and solids content monitored for solids rise above specified acceptable limits. Additionally the binder temperature is controlled with a reservoir as a depository for temperature controlled binder and attached to the furnace are spraying arms one with the ability to spray binder, binder species, and aqueous solutions on the fiberglass, with a secondary spraying assembly capable of spraying aqueous solutions on a rotating drum and on roller assemblies. The secondary arm sprays aqueous solutions in a specified width at least (4 inches) but no greater than the width of the swath of fiberglass exiting the bushing plate.

In some instances styrene resin for composite applications is mixed with other additives such as polybutene by a shear mixer and temperature controlled with heating and cooling coils in the storage tank. PH is monitored and the tank is continually agitated to ensure complete mixing of the styrene without heat or cool spots occurring in both the storage and dispensing tanks. Styrene percent solids are continually monitored.

Water is conditioned soft and in some cases the water is mixed with the resin creating an aqueous solution or the water which may is sprayed onto resin as it is applied to a rotating drum to control the moisture level of the resulting fiberglass mat formed. Additionally, the water is utilized as a spray, fog or rolled onto the expanded fiberglass mat before it enters a curing process.

Glass Melting Furnace (18)

The glass melting process involves the use of natural gas and combustion air mixtures controlled by a feedback loop from a flame temperature sensor (20). The air/fuel mixture can be controlled manually to the burner assembly, if necessary and for system start-up and shut-off. The molten glass level is controlled to maintain a minimum level in the furnace (18) based on a set point controller (26). Once the set point controller's (26) minimum is reached more glass is automatically fed to the furnace by the glass hopper (10) to a vibrator (14) mounted under the stationary glass feeder (12) all of which is controlled by a feedback loop from the set point controller (26). The furnace (18) is mounted on a traverse cart (22) with track (24).

Bushing Plate (28), Orifices (36), Orifice Tip (38) and Cooling Coil (32) Assembly (42)

Molten glass exits the furnace (18) through an Inconel bushing plate (28) in one of various bushing plate configurations, in continuous strand filaments of approximately 25 to 35 microns in diameter, depending on the final product specifications desired, one or the other bushing plate configuration is used as specified in various custom client configurations. Cooling is accomplished through a Bushing Cooling Loop Assembly and Controller (32) with cooling coils of a 3 inch width and 15 inches long mounted directly under the Inconel bushing plate (28) in a race track pattern. Additionally design changes are accomplished through varying bushing plate (28) designs and further orienting the bushing plate (28) so that the bushing plate (28) is at a near perpendicular angle to the length of the drum at a minimum 6 degrees relative (30), along the longitudinal axis of the drum. Shields (34) are mounted under the bushing plate (28) at either side to prevent room air flow from disrupting the fall of continuous strands through the Inconel bushing plate (18) to the drum below.

Bushing plate (28) orifices (36) have an orifice size measured in a drill size and machine bit referred to as a 27 drill which is the finest. The tip (38) with the largest size of an orifice is the 10 drill, in this aspect, the orifice tip (38) sizes have alternating hole sizes which are at least a 7 row plate, with another control at the 8-9 row plate orifice patterns (40) of orifice sizes (36), width of the row of orifice tip (38) holes as being in the range of 7-10 row, with the 7 row plate being 298 holes and the largest being a 10 row plate which is 425 tip hole. Patterns are such as to leave a space (86) of 0.500″ between two sections of bushing plate (28) orifice tips (38) creating orifice tip patterns (40). The filaments exiting from the orifices of the bushing plate (28) wrap onto the rotating drum at a 6 degree relative angle (30) to the longitudinally and circumferentially enlarged drum providing for more efficient operation and control. The bushing plate (28) forces the exiting molten fiberglass filament onto the drum at a relative angle of 6 degrees (30) plus or minus 1 degree from perpendicular to the axis of the drum altering the relative position of the exiting filament to the rotating drum and the orientation of the orifices based on the configuration and orientation of the bushing plate (28) relative to the drum.

Immediately below the bushing plate (28) and attached to the furnace (18) is a cooling water coil (32) part of the bushing cooling loop assembly (42) that together with pressure controls for monitoring clogging and temperature and water pressure control make up the bushing cooling loop assembly (42) that cools the continuous filament strands to a temperature that is cool to the touch, slightly above ambient temperature. The cooling water is supplied either by chiller or from constant temperature water well. Pressure sensors detect if the cooling water loop is becoming clogged by particulates. Temperature sensors provide feedback to the chiller to control temperatures of the bushing cooling loop assembly (42). The bushing cooling loop assembly (42) consists of 7 quarter inch copper tubes wrapped around the bottom of the furnace (18) against the bushing plate (28). These cooling coils (32) are looped in a racetrack (rectangular) pattern within 1 inch of the bushing plate (28). The bushing cooling loop assembly (42) executes a loop that is 15 inches long and 3 inches wide at its inside diameter. One coil is an air coil that is ⅜ inch copper tubing with an air/water in and water exiting the bushing cooling loop assembly at an 80 degree angle. The shields (34) previously mentioned are placed around the area just below the bushing plate (28) and attached to the furnace (18) to control the ambient air movement and air movement generated by the rotating drum or by the traverse of the furnace on the traverse cart (22). The shields (34) prevent excessive air movement from causing the glass continuous stranded filaments to collide. The bushing cooling loop assembly (42) cools the fibers as they exit orifice tips (38) of the orifices of the bushing plate (28). Cooling is accomplished by pumping water through the loops such that the running water cools the filaments in a specified timeframe bringing those filaments to room temperature.

Rotating Drums and Traversing (44) Melt Furnace

The rotating drums are wrapped in plastic sheeting to enable the mat's removal from the drum. Once the plastic sheeting wraps the drum, a thin application of mold release oil is applied to the surface of the sheeting. As the filament strands fall from the bushing plate (28) an operator assists the process in attaching the falling filament strands of molten glass to the plastic sheeting wrapped drum. Additionally, the operator may assist in reattaching filaments that have detached from the rotating drum and reattach as necessary. The rotating drum is circumferentially and longitudinally superior in size with a substantial and sustainable control of the rotation of the drum to control the speed of layering of fiberglass upon the rotating drum.

The furnace traverse (44) of the drum's length repeatedly following a specified longitudinal continuous path covering the drum with a layer of fiberglass along the traverse track (46) with the traverse cart (22). In one embodiment as the glass is applied to the drum, a resin mixture (48) sprayed from a resin arm attached to the traverse and water sprayed from a water arm (50) attached to the traverse are sprayed onto the fiberglass on the drum by nozzles of both the resin and water spray situated and aimed at the back of the drum. The spray nozzles are linked to the movement of the furnace traverse and the spray nozzles traverse the back of the drum in synchronicity with the traverse of the furnace (44) across the drum at least 4 inches in width but in no case wider than the width of the falling fiberglass filaments in one embodiment no more than 4 inches in width. Physical elements of the process are controlled by a computer machine and software program controlling the number and speed of furnace movement or furnace traverse (44), rotation speed of the drum, and application of resin spray mixture arm (48) from first one arm and/or water spray mixture arm (50) and from a second arm. The computer's control of these parameters through a software program and control of these variables and operating parameters permits the mat to have progressive densities when expanded. As the filaments are spun onto the rotating drum and the melt furnace or furnace traversing (44) following the traverse track (46) and its relative position in relation to the drum below then the drum can be sprayed with an aqueous solution from a first arm attached to the traverse of the furnace as the furnace traverses the drum or a first arm or a second arm, mounted on the traverse that sprays binder (or binder species composed essentially of binder, chemical additives, and water or aqueous solutions) onto the back side of the rotating drum as the furnace traverse the drum following the traverse track (46). Temperature control system of the binder in the reservoir is accomplished to within + or −10% of 70 degrees Fahrenheit. The temperature controlled binder or combination binder species may be sprayed onto the rotating drum in tandem with an aqueous solution.

The mat article is complete when a total weight measurement of glass fiber, resin mixture and water has reached the weight prescribed in the formulation of each specific product. Attainment of the product specific weight can be controlled in some cases by load cells (52) or by calculating the time necessary for that product specific weight to be attained. The formula of the load cell weight control is achieved by taking the weight of the fibers on the drum adding the weight of the resin and subtracting the weight of the drum. When the mat reaches its product specific weight, the spinning of the drum is complete and the operator actuates the braking mechanism on the drum drive. The drum has a V-shaped slot (54) that runs longitudinally parallel to the axis of rotation of the drum from one end to other across the width of the drum and thereby across the width of the continuous strand filament mat laying thereupon. The operator uses this slot to cut the mat from the drum. At this point the mat is promptly removed from the drum, laid on a flat surface covered with plastic sheeting; from there the mat is rolled onto a steel bar in a direction perpendicular to the axis of rotation of the drum. The weight of the mat is confirmed and recorded by weighing the rolled mat and calculating the net rolled mat weight.

Let-Off Table: Entry and Exit

The rolled mat is transported to the Let-Off Table which is a slow moving conveyor slightly larger than the unrolled mat. The mat is unrolled onto the moving conveyor and the top layer of plastic is removed. The unrolling process requires that the mat be unrolled with no creases or folds, straight with its edges equidistant from the sides of the conveyor; otherwise the unrolled mat will not expand properly. The resin coating the glass strands is heated from above and below to soften the resin. As the leading edge of the unrolled mat emerges beyond the exit edge of the conveyor, the leading edge of the mat is guided through water spray rollers and onto a bottom conveyor chain of the curing oven using a guide rope attached to the leading edge. The curing oven's bottom conveyor chain pulls the mat into the oven. As each mat exits the Let-Off table it is attached with ropes to the end of the mat ahead of it so successive mats are continuously drawn into the curing oven. The ropes are used to connect mats because ropes do not damage the slitter knives used later in the process.

Media Upper and Lower Skin Control Assembly with Water Spray for Bowed and Straight Rollers

The water spray (56) onto the rollers of the upper (58) and lower (60) skin control assembly controls operating parameters creating various densities of the top and bottom surface skinning or skins and to a certain extent the stiffness of the final finished fiberglass product. As the mat is drawn into the oven, it first passes through the upper (58) and lower (60) skin control assembly's rollers which have a series of metal rollers with water sprays (56) associated with them. For some products straight (66) rollers are used with upper (74) and lower (76) separately controlled drive assemblies and for other products curved or bowed (68) rollers are used. For some products water spray (56) is fogged (70) directly onto the expanded mat as it passes over or under the rollers. For other products water spray (56) is fogged (70) onto the top or the bottom of the rollers so that water is indirectly applied to the top or the bottom of the mat through first being applied to the top or the bottom of the rollers. The water spray (56) is part of the Media

Upper and Lower Skin Control Assembly and are mounted on rolling casters so various combinations and embodiments of the water spray (56) rollers of the Media Upper and Lower Skin Control Assembly (65) can be inserted into the process as needed. Additionally, each media upper and lower skin control assembly (65) may have a separate integrated catch basin (72) attached to capture excess water from the spraying process.

Curing Oven (88) and Oven Conveyor Assembly (80 and 86), Multi-zoned Interior (84) and Controller (82)

The operating parameters of the oven determine the weight per square foot, the loft, the compressive strength and to some extent the stiffness of the final product and are controlled by a curing oven controller with computer and software (82). The speed of upper (80) rollers of conveyor chain is regulated according to a precise formula at a speed slightly different than the speed of oven's lower (86) rollers of the conveyor chain which controls the speed of the expanded mat as it travels through the interior (84) of the oven on the conveyor chain. The interior (84) of the oven is multi-temperature zoned. The shut-off switch in the controller (82) for the rollers (80, 86) is electrically linked and integrated with the oven's conveyors so that both start-up and shut-down simultaneously at the controller (82).

As the mat is drawn into interior (84) of the oven operators expand the mat to the proper width for the product being made. The upper (80) rollers of the conveyor chain of the curing oven are set to a specific height for each product to set the loft (i.e. the height) of the expanded fiberglass. The speed of the upper (80) rollers of the conveyor chain is regulated according to a precise formula at a speed slightly different from the speed of the oven's lower (86) rollers of the conveyor chain which controls the speed of the expanded mat as it travels through the oven.

The temperatures of the multiple heating zones in the curing oven interior (84) are set by oven operation to an appropriate temperature for the product being cured at the controller (82).

Accumulator and Windup Machine

As the cured mat exits the oven, it is drawn into a set of accumulator rollers, initially by the rope threaded through the accumulator assembly by operator assist and onto the windup section where it is wound onto a cardboard core Immediately after exiting the oven, the expanded mat passes over a roller where it is cut by circular roller knives, cutting off the uneven outside edges and slitting the mat into rolls of the prescribed product dependent widths. After the rolls reach the appropriate length on the windup cores, the operator stops the rolling process and then the operator intervenes to cut the wound mat from the larger roll. The accumulator section allows the rest of the mat to continue traveling through the oven while the rolls of finished product are removed from the windup section and new cores are put in place. The leading edge of the next section of the mat is then attached to new windup cores and the operator actuates the accumulator to resume feeding the slit rolls onto the cardboard cores.

Quality Control Equipment

Quality of finished product is maintained through an extensive process of inline and post quality control process steps including measuring loft and roll width utilizing a quality control fixture which measures loft and roll width, through another fixture that cuts out single square foot samples, while another fixture is used to measure the compressive strength of a square foot sample. Each square foot sample is weighed. Additionally the top and the bottom skin of a sample are removed and the scale is used to determine the percentage by weight of the skin on the top surface the percentage by weight of the skin on the bottom surface.

Description of One Embodiment for Progressive Density Mat

FIG. 1 is a side cutaway view of a melting furnace with natural gas flame and a glass feeder hopper mechanism, stationary glass feeder, and vibrator, secondary chute into the traversing melter furnace, showing the traverse cart, the track and the set point controller. This figure details the relative position of the various main components of the melting furnace and its traverse mechanism, with glass hopper (10), glass feeder (12), vibrator (14), to a secondary chute (16), a melt furnace (18) a flame temperature sensor (20) and a traverse cart (22) for traversing the melter furnace with track (24) and set point controller (26) for feeding more glass in the melter furnace.

FIG. 6 demonstrates the relative position of the falling fibers exiting the bushing plate and falling onto the rotating drum, as well as demonstrating the position of the binder spray head and aqueous solutions spray head relative to the traversing melter and the rotating drum of FIG. 5. This figure also indicates the relative angle of traverse of the melter furnace.

FIG. 8 is an end view of straight rollers and their associated water spray nozzles and arrow showing direction of travel of fiberglass and controls media upper and lower skin which is composed of a high pressure dual pumping system, each of which provides water sprays either on the rollers or the media from either Pump A (56) to the top side of the top roller or Pump B (64), typically spraying water from Pump B to the underside of the rollers. Top rollers (58) are adjustable and separately driven with respect to bottom coasting rollers (62), with multiple spray heads from each adjustable spray head assembly. Bottom rollers (60) are adjustable and separately driven from the top rollers (58). (65) is the total assembly from top to wheels.

FIG. 9 End view of bowed rollers and associated water sprays and arrow indicating direction of travel of the fiberglass are sprayed with water fog nozzles (70). Attached to and integrated with the portable Bowed Roller Assembly is a catch basin (72) deleted for clarity that captures the water fogged onto the rollers from above and below.

FIG. 17 Top view of bowed rollers a straight roller (66) that first engages the mat to three bowed rollers (68) that engages the mat and is used to maintain width expansion consisting of a straight roller (66) that first engages the mat to three bowed rollers (68). The top view shown first slides over straight roller in the direction of travel of the mat in a clockwise direction over the top of the roller and then under the second roller which is bowed (first in a series of bowed rollers) (68) in a counterclockwise direction and then over the top of the third roller which is bowed in a clockwise direction, and then under the fourth roller, bowed in a counterclockwise direction, the movement of the mat over and under the rollers provides for linear expansion of the mat. The three bowed rollers each of which is (68) are sprayed across the span of the bowed rollers both above and below. Shown are the straight roller and the three bowed rollers. Note the angular rotation of the individual rollers in the roller assembly identifies the key components, the three bowed rollers following the single straight roller, in this embodiment for progressive density mats.

Generally, in another aspect, a method of forming a fiberglass mat, having the steps of feeding a fiberglass media or mat between bowed (68) or straight (66) rollers of the roller assembly apparatus driven by drive assemblies (74) for both upper and lower rollers that are separately driven providing for a differential pressure across the mat reducing weight variation across the web as it is fed into the curing oven but allowing for control of the density in a progressive manner, which is referenced in this aspect as expanding the mat. Bowed rollers are to optimize the stretch of the fiber mat to apply water to the mat. Weight variation is improved from +/−20% to +/−5% across the finished expanding mat, with consistent water content and an improved top and bottom skinning or surface formation.

In some embodiments the relative pattern of the glass fibers fed onto the rotating drum is adjusted by the orientation of the bushing plate (28) and the orifices (36) thereby.

In another embodiment load cells (52) are utilized to decrease weight variations of the fiberglass media as mat. Load cells (52) increase accuracy of the final weight over that of other techniques improving product quality weight accuracy from +/−20%, to +/−5%.

In another embodiment applying water by water spray nozzles (50) onto a flat mat surface applies the water more consistently resulting in higher quality skins.

In other embodiments, water is applied to the binder as it is applied to the fiberglass and/or is applied to the fiberglass mat as the binder is applied to the fiberglass mat controlling the moisture to a targeted moisture level plus or minus 2.5%.

In another embodiment binder species temperature range is controlled to 72 degrees Fahrenheit + or −10%.

All systems are controlled and configured with a software program integrally operating upon a computer machine.

Since other modifications and changes varied to fit particular operating requirements and environments will be apparent to those skilled in the art, the invention is not considered limited to the example chosen for purposes of disclosure, and covers all changes and modifications which do not constitute departures from the true spirit and scope of this invention. For instance there are embodiments that include only straight rollers for expansion of the fiber mat, and some where water fog nozzle sprays water on the rollers, and in other cases a water spray head wets the rotating drum prior to wrap the fiberglass on the rotating drum.

Having thus described the invention, what is desired to be protected by Letters Patent is presented in the subsequently appended claims. 

What is claimed is:
 1. An improved system and method for continuous strand fiberglass media manufacturing, comprising: means for melting glass efficiently; means for supporting the orifices, rigidly connected to said means for melting glass efficiently; means for exiting molten glass as filaments, rigidly connected to said means for supporting the orifices; means for receiving fiberglass, cooperatively connected to said means for exiting molten glass as fibers; means for spraying binder, binding species and aqueous solutions on fiberglass, operationally connected to said means for receiving fiberglass; means for positioning of bushing plate at a 6 degree angle from perpendicular to the axis of the rotating drum, rigidly connected to said means for spraying binder, binding species and aqueous solutions on fiberglass, and operationally connected to said means for melting glass efficiently; means for cooling fibers with water, rigidly connected to said means for supporting the orifices; means for stabilizing fibers from the let-off table prior to entry into the bowed rollers, successively connected to said means for receiving fiberglass; means for spreading fibers counterclockwise, sequentially connected to said means for stabilizing fibers from the let-off table prior to entry into the bowed rollers; means for spreading fibers clockwise, sequentially connected to said means for rotating fibers counterclockwise; means for spreading fibers in a counterclockwise rotation, sequentially connected to said means for spreading fibers clockwise; means for fogging the fiberglass moving across the rollers with water, tangentially connected to said means for spreading fibers in a counterclockwise rotation, tangentially connected to said means for spreading fibers clockwise, and tangentially connected to said means for spreading fibers counterclockwise; means for weighing the fiberglass, operationally connected to said means for receiving fiberglass; and means for controlling weight variations across the fiberglass through an analysis of differential pressure, operatively connected to said means for weighing the fiberglass.
 2. The improved system and method in accordance with claim 1, wherein said means for melting glass efficiently comprises a traversing, enlarged temperature control melter.
 3. The improved system and method in accordance with claim 1, wherein said means for supporting the orifices comprises a bushing plate.
 4. The improved system and method in accordance with claim 1, wherein said means for exiting molten glass as fibers comprises an orifice.
 5. The improved system and method in accordance with claim 1, wherein said means for receiving fiberglass comprises an enlarged circumference, enlarged length rotating drum.
 6. The improved system and method in accordance with claim 1, wherein said means for spraying binder, binding species and aqueous solutions on fiberglass comprises two spray heads.
 7. The improved system and method in accordance with claim 1, wherein spray width is at least 4 inches but no greater than the width of the falling fiberglass filaments exiting the bushing plate.
 8. The improved system and method in accordance with claim 1, wherein said means for positioning of bushing plate slightly off perpendicular at a relative angle of 6 degrees to the axis of the rotating drum comprises a traversing melter furnace assembly with a slanted bushing plate.
 9. The improved system and method in accordance with claim 1, wherein said means for cooling fibers with water comprises a cooling coil, rectangular bushing cooling loop assembly.
 10. The improved system and method in accordance with claim 1, wherein said means for stabilizing fibers from the let-off table prior to entry into the bowed rollers comprises a straight roller.
 11. The improved system and method in accordance with claim 1, wherein said means for spreading fibers counterclockwise comprises a counterclockwise rotation of a first bowed roller.
 12. The improved system and method in accordance with claim 1, wherein said means for spreading fibers clockwise comprises a clockwise rotation of a second bowed roller.
 13. The improved system and method in accordance with claim 1, wherein said means for spreading fibers in a counterclockwise rotation comprises a counterclockwise rotation of a third bowed roller.
 14. The improved system and method in accordance with claim 1, wherein said means for fogging the rollers and roller assembly with water comprises a water fog nozzle.
 15. The improved system and method in accordance with claim 1, wherein said means for weighing the fiberglass on the rotating drum comprises a load cell.
 16. The improved system and method in accordance with claim 1, wherein said means for controlling weight variations across the fiberglass comprises a strain gage.
 17. The improved system and method in accordance with claim 1, wherein said means for controlling skin characteristics and progressive densities across the fiberglass mat comprises bowed and straight rollers.
 18. An improved system and method for continuous strand fiberglass media manufacturing, comprising: a reservoir for controlling temperature of binder; a traversing, enlarged, temperature control melter, for melting glass efficiently; a bushing plate, for supporting the orifices, rigidly connected to said melter; an orifice, for exiting molten glass as fibers, rigidly connected to said bushing plate; an enlarged circumference, enlarged length rotating drum, for receiving fiberglass, cooperatively connected to said orifice; a first sprayer for spraying binder and binding species, operationally connected to said rotating drum; a second sprayer for spraying aqueous solutions, operationally connected to said rotating drum; a traversing melter furnace assembly, for positioning of a bushing plate at a 6 degree angle to the axis of the rotating drum, rigidly connected to said first sprayer and said second spray, and operationally connected to said melter; a bushing cooling loop assembly, for cooling fibers with water, rigidly connected to said bushing plate; a straight roller, for stabilizing fibers from the letoff table prior to entry into the bowed rollers, successively connected to said rotating drum; a counterclockwise rotation first bowed roller, for spreading fibers counterclockwise, sequentially connected to said straight roller; a clockwise rotation second bowed rollers, for spreading fibers clockwise, sequentially connected to said first bowed roller; a counterclockwise rotation of a third bowed rollers, for spreading fibers in a counterclockwise rotation, sequentially connected to said second bowed rollers; a water fog nozzle, for fogging rollers with water, cooperatively connected to a first roller, and/or cooperatively connected to a second roller, and/or cooperatively connected to a third roller; a load cell, for weighing the fiberglass, operationally connected to said rotating drum; and a strain gage, for controlling weight variations across the fiberglass through an analysis of differential pressure, operatively connected to said load cell.
 19. An improved system and method for continuous strand fiberglass media manufacturing, comprising: a traversing, enlarged, temperature control melter, for melting glass efficiently; a bushing plate, for supporting the orifices, rigidly connected to said melter; an orifice, for exiting molten glass as fibers, rigidly connected to said bushing plate; a hollow, enlarged circumference, enlarged length rotating drum, for receiving fiberglass, cooperatively connected to said orifice; a sprayer, for spraying binder, binding species and aqueous solutions on fiberglass, operationally connected to said rotating drum; a traversing melter furnace assembly, for positioning of bushing plate at an angle 6 degrees from perpendicular to the axis of the rotating drum, rigidly connected to said sprayer, and operationally connected to said melter; a cooling coil, rectangular bushing cooling loop assembly, for cooling fibers with water, rigidly connected to said bushing plate; a straight roller, for stabilizing fibers from the let-off table prior to entry into the bowed rollers, successively connected to said rotating drum; a counterclockwise rotation first bowed roller, for spreading fibers counterclockwise, sequentially connected to said straight roller; a clockwise rotation second bowed rollers, for spreading fibers clockwise, sequentially connected to said first bowed roller; a counterclockwise rotation third bowed rollers, for spreading fibers in a counterclockwise rotation, sequentially connected to said second bowed rollers; a water fog nozzles, for fogging rollers with water, thermally connected to a third bowed rollers, thermally connected to a second bowed rollers, and thermally connected to a first bowed roller; a load cell, for weighing the fiberglass, operationally connected to said rotating drum; and a strain gage, for controlling weight variations across the fiberglass through an analysis of differential pressure, operatively connected to said load cell. 